Simple approach to precisely 02 consumption, and anesthetic absorption during low flow anesthesia

ABSTRACT

A process for determining gas(x) consumption, wherein said gas(x) is selected from; a) an anesthetic such as but not limited to; i) N 2 O; ii) sevoflurane; iii) isoflurane; iv) halothane; v) desflurame; or the like b) Oxygen (O 2 ).

FIELD OF THE INVENTION

This invention relates to a method of intraoperative determination of O₂ consumption ({dot over (V)}O₂) and anesthetic absorption (VN₂O among others), during low flow anesthesia to provide information regarding the health of the patient and the dose of the gaseous and vapor anesthetic that the patient is absorbing. In addition to the monitoring function, this information would allow setting of fresh gas flows and anesthetic vaporizer concentration such that the circuit can be closed in order to provide maximal reduction in cost and air pollution.

The method provides an inexpensive and simple approach to calculating the flux of gases in the patient using information already available to the anesthesiologist The {dot over (V)}O₂ is an important physiologic indicator of tissue perfusion and an increase in {dot over (V)}O₂ may be an early indicator of malignant hyperthermia. The {dot over (V)}O₂ along with the calculation of the absorption/uptake of other gases would allow conversion to closed circuit anesthesia (CCA) and thereby save money and minimize pollution of the atmosphere.

BACKGROUND OF THE INVENTION

A number of techniques exist which may be utilized to determine various values for oxygen flow or the like. Current methods of measuring gas fluxes breath-by-breath are not sufficiently accurate to close the circuit without additional adjustment of flows by trial and error. These prior techniques are set out below in the appropriate references. In the past many attempts have been made to measure VO₂ during anesthesia. The methods can be classified as:

-   1) Empirical formula based on body weight e.g.,     -   a) The Brody equation (1) {dot over (V)}O₂=10*BW^(3/4) is a         ‘static’ equation that cannot take into account changes in         metabolic state. -   2) Determination of oxygen loss (or replacement) in a closed system     -   Severinghaus (2) measured the rate of N₂O and O₂ uptake during         anesthesia. Patients breathed spontaneously via a closed         breathing circuit (gas enters the circuit but none leaves). The         flow of N₂O and O₂ into the circuit was continuously adjusted         manually such that the total circuit volume and concentrations         of O₂ and N₂O remain unchanged over time. If this is achieved,         the flow of N₂O and O₂ will equal the rate of N₂O and O₂ uptake.     -   Limitations: Unsuitable for clinical use.         -   1. Method only works with closed circuit, which is seldom             used clinically.         -   2. Requires constant attention and adjustment of flows. This             is incompatible with looking after other aspects of patient             care during surgery.         -   3. The circuit contains a device, a spirometer, that is not             generally available in the operating room.         -   4. Because the spirometer makes it impossible to             mechanically ventilate patients, the method can be used only             with spontaneously breathing patients.         -   5. Method too cumbersome and imprecise to incorporate             assessment of flux of other gases that are absorbed at             smaller rates, such as anesthetic vapors. -   3) Gas collection and measurement of O₂ concentrations:     -   a) Breath-by-breath: measurement of O₂ concentration and         expiratory flows at the mouth         -   For this method, one of the commercially available metabolic             carts can be attached to the patient's airway. Flow and gas             concentrations are measured breath-by-breath. The device             keeps a running tally of inspired and expired gas volumes.     -   Limitations:         -   1. Metabolic carts are expensive, costing US             $30,000-$50,000.     -   2. The methods they use to measure O₂ flux (VO₂) are fraught         with potential errors. They must synchronize both flow and gas         concentration signals. This requires the precise quantification         of the time delay for the gas concentration curve and         corrections for the effect of gas mixing in the sample line and         time constant of the gas sensor. The error is greatest during         inspiration when there are large and rapid variations in gas         concentrations. We have not found any reports of metabolic carts         used to measure {dot over (V)}O₂ during anesthesia with         semi-closed circuit         -   3. Metabolic carts do not measure fluxes in N₂O and             anesthetic vapor.         -   Our method measures flux of O₂ (VO₂), N₂O (VN₂O), and             anesthetic vapor (VAA) with a semi-closed anesthesia circuit             using the gas analyzer that is part of the available             clinical set-up.     -   b) Collecting gas from the airway pressure relief (APL) valve         and analyzing it for volume and gas concentration. This will         provide the volumes of gases leaving the circuit This can be         subtracted from the volumes of these gases entering the circuit.         This requires timed gas collection in containers and analysis         for volume and concentration.     -   Limitations         -   i) The gas containers, volume measuring devices, and gas             analyzers are not routinely available in the operating room.         -   ii) The measurements are labor-intensive, distracting the             anesthetist's attention from the patient. -   4) Tracer gases     -   Henegahan (3) describes a method whereby argon (for which the         rate of absorption by, and elimination from, the patient is         negligible) is added to the inspired gas of an anesthetic         circuit at a constant rate. Gas exhausted from the ventilator         during anesthesia is collected and directed to a mixing chamber.         A constant flow of N₂ enters the mixing chamber. Gas         concentrations sampled at the mouth and from the mixing chamber         are analyzed by a mass spectrometer. Since the flow of inert         gases is precisely known, the concentrations of the inert gases         measured at the mouth and from the mixing chamber can be used to         calculate total gas flow. This, together with concentrations of         O₂ and N₂O, can be used to calculate the fluxes of these gases.

This method uses the principles of the indicator dilution method. It requires gases, flowmeters, and sensors not routinely available in the operating room, such as argon, N₂, precise flowmeters, a mass spectrometer, and a gas-mixing chamber.

-   5) {dot over (V)}O₂ from variations of the Foldes (1952) method:     ${{Foldes}\quad{formula}\text{:}F_{I}O_{2}} = \frac{{O_{2}{flow}} - {VO}_{2}}{{FGflow} - {VO}_{2}}$     -   Where FIO₂ is the inspired fraction of O₂; O₂flow is the flow         setting in ml/min (essentially equivalent to VO₂); VO₂ is the O₂         uptake as calculated from body weight and expressed in ml/min         (essentially equivalent to VO₂); and FG flow is the fresh gas         flow (FGF) setting in ml/min.     -   a) Biro (4) reasoned that since modern sensors can measure         fractional airway concentrations, the Foldes equation can be         used to solve for VO₂.         ${\overset{.}{V}O_{2}} = \frac{{O_{2}{flow}} - \left( {F_{I}O_{2}*{FGflow}} \right)}{1 - {F_{I}O_{2}}}$         where FGflow and O₂flow are obtained from the settings of the         flowmeters. -   Drawbacks of the approach:     -   1. This approach requires knowing the FIO₂. FIO₂ varies         throughout the breath and must be expressed as a flow-averaged         value. This requires both flow sensors and rapid O₂ sensors at         the mouth; it therefore has the same drawbacks as the metabolic         cart type of measurements.     -   2. Even if FIO₂ can be measured and timed volumes of O₂         calculated, its use in the equation given in the article is         incorrect for calculating VO₂. Biro calculated VO₂ of 21         patients during elective middle ear surgery using his         modification of the Foldes equation. His calculations were         within an expected range of VO₂ as calculated from body weight         but he did not compare his calculated VO₂values to those         obtained with a proven method. Recently Leonard et al (5)         compared the VO₂ as measured by the Biro method with a standard         Fick method in 29 patients undergoing cardiac surgery. His         conclusion was the Biro method is an “unreliable measure of         systemic oxygen uptake” under anesthesia. We also compared the         VO₂ as calculated by the Biro equation with our data from         subjects in whom VO₂ was measured independently and found a poor         correlation.     -   b) Viale et al (6) calculated VO₂ from the formula         VO₂=VE*(FIO₂*FEN₂/FIN₂−FEO₂)     -   Where FIO₂ and FEO₂ are inspired and expired fractional         concentrations of O₂, respectively; FIN₂ and FEN₂ are inspired         and expired N₂ fractional concentrations, respectively.     -   The method requires equipment not generally available in the         operating room—a flow sensor at the mouth to calculate VE and a         mass spectrometer to measure FEN₂ and FIN₂. Furthermore, it is         then like the breath-by-breath analyzers in that means must be         provided to integrate flows and gas concentrations in order to         calculate flow-weighted inspired concentrations of O₂ and N₂.     -   c) Bengston's method (7) uses a semi-closed circle circuit with         constant fixed fresh gas flow consisting of 30% O₂ balance N₂O.         VO₂ is calculated as         {dot over (V)}O₂={dot over (V)}fgO₂−0.45({dot over         (V)}fgN₂O)−(kg: 70.1000.t ^(−0.5)))         where {dot over (V)}fgO₂ is oxygen fresh gas flow; {dot over         (V)}fgN₂O is the N₂O fresh gas flow and kg is the patient weight         in kilograms. The method was validated by collecting the gas         that exited the circuit and measuring the volumes and         concentrations of component gases.     -   Limitations of the method:         -   i) N₂O absorption/uptake is not measured but calculated from             patient's weight and duration of anesthesia.         -   ii) The equation is valid only for a fixed gas concentration             of 30% O₂, balance N₂.         -   iii) The validation method requires collection of gas and             measurement of its volume and gas composition. -   6) Anesthetic absorption/uptake predicted from pharmacokinetic     principles and characteristics of anesthetic agent     -   a) The equation described by Lowe H J. The quantitative practice         of anesthesia. Williams and Wilkins. Baltimore (1981), p 16         {dot over (V)}AA=f*MAC*λ_(B/G) *Q*t ^(−1/2)         -   where VAA is the uptake of the anesthetic agent, f*MAC             represents the fractional concentration of the anesthetic as             a fraction of the minimal alveolar concentration required to             prevent movement on incision,, λ_(B/G) is the blood-gas             partition coefficient, Q is the cardiac output and t is the             time.         -   Limitations:         -   i) In routine anesthesia, cardiac output (Q) is unknown.         -   ii) The formula is based on empirical averaged values and             does not necessarily reflect the conditions in a particular             patient. For example, it does not take into account the             saturation of the tissues, a factor that affects VAA.     -   b) Lin C Y. (8) proposes the equation for uptake of anesthetic         agent ({dot over (V)}AA)         {dot over (V)}AA={dot over (V)}A*FI*(1−FA/FI)         Where {dot over (V)}AA is the uptake of the anesthetic agent; VA         is the alveolar ventilation, FA is the alveolar concentration of         anesthetic, and FI is the inspired concentration of anesthetic.     -   Limitations:     -   i) This formula cannot be used as VA is unknown with low flow         anesthesia;     -   ii) FI is complex and may vary throughout the breath so a         volume-averaged value is required.     -   iii) FI is not available with standard operating room analyzers. -   7) Calculations directly from invasively-measured values     -   a. Pestana (9) and Walsh (10) placed catheters into a peripheral         artery and into the pulmonary artery. They used the oxygen         content of blood sampled from these catheters and the cardiac         output as measured by thermodilution from the pulmonary artery         to calculate VO₂. They compared the results to those obtained by         indirect calorimetry.     -   Limitations     -   i) The method uses monitors not routinely available in the         operating room.     -   ii) The placement of catheters in the vessels has associated         morbidity and cost.

Summary Table Measures Can Uses gas not Based on measure Standard Requires expired available Wrong prediction absorp

ion Anesthetic Additional additional gas on clinical Uses assumptions from of other Circuit Manipulation measurements collection monitor “F₁O₂” or equation pooled data anesth

tic Empirical Brody Yes body No formula weight needed Severinghaus No. Uses Yes. Yes. Yes No closed Constant Circuit circuit adjustment volume of flow Metabolic Yes. Flow Yes Yes No carts at the mouth. Timed gas No. Yes. Yes Yes, Yes collection Volume. volumes Tracer Vaile No. Yes. Yes Yes, Yes Yes- No gases Inserted {dot over (V)}_(β) —N₂ assumes nonre- RQ breathing valve to separate gases Heneghan Yes. Yes Yes. Yes Possib

y Foldes Biro Yes Yes No Bengson No. Yes. Yes-only Yes- No. For valid for weight validation fixed inspired gas ratio Pharmco- Lowe Yes. Yes Yes Yes Yes. kinetic {dot over (Q)}-time principles Lin Yes. {dot over (V)}_(A) Yes Yes No

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REFERENCE LIST Reference List

-   (1) Brody S. Bioenergetics and Growth. New York: Reinhold, 21945. -   (2) Severinghaus J W. The rate of uptake of nitrous oxide in man. J     Clin Invest 1954; 33:1183-1189. -   (3) Heneghan C P, Gillbe C E, Branthwaite M A. Measurement of     metabolic gas exchange during anaesthesia. A method using mass     spectrometry. Br J Anaesth 1981; 53(1):73-76. -   (4) Biro P. A formula to calculate oxygen uptake during low flow     anesthesia based on FIO2 measurement. J Clin Monit Comput 1998;     14(2):141-144. -   (5) Leonard I E, Weitkamp B, Jones K, Aittomaki J, Myles P S.     Measurement of systemic oxygen uptake during low-flow anaesthesia     with a standard technique vs. a novel method. Anaesthesia 2002;     57(7):654-658. -   (6) Viale J P, Annat G J, Tissot S M, Hoen J P, Butin E M, Bertrand     O J et al. Mass spectrometric measurements of oxygen uptake during     epidural analgesia combined with general anesthesia. Anesth Analg     1990; 70(6):589-593. -   (7) Bengtson J P, Bengtsson A, Stenqvist O. Predictable nitrous     oxide uptake enables simple oxygen uptake monitoring during low flow     anaesthesia. Anaesthesia 1994; 49(1):29-31. -   (8) Lin C Y. [Simple, practical closed-circuit anesthesia]. Masui     1997; 46(4):498-505. -   (9) Pestana D, Garcia-de-Lorenzo A. Calculated versus measured     oxygen consumption during aortic surgery: reliability of the Fick     method. Anesth Analg 1994; 78(2):253-256. -   (10) Walsh T S, Hopton P, Lee A. A comparison between the Fick     method and indirect calorimetry for determining oxygen consumption     in patients with fulminant hepatic failure. Crit Care Med 1998;     26(7):1200-1207. -   11. Baum J A and Aitkenhead R A. Low-flow anaesthesia. Anaesthesia     50 (supplement): 37-44, 1995

OBJECTS OF THE INVENTION

It is therefore a primary object of this invention to provide an improved method of intraoperative determination of O₂ consumption ({dot over (V)}O₂) and anesthetic absorption (VN₂O, among others), during low flow anesthesia to provide information regarding the health of the patient and the dose of the gaseous and vapor anesthetic that the patient is absorbing.

It is yet a further object of this invention to provide, based on determination of O₂ consumption ({dot over (V)}O₂) and anesthetic absorption (VN₂O, among others), the setting of fresh gas flows and anesthetic vaporizer concentration such that the circuit can be substantially closed in order to provide maximal reduction in cost and air pollution.

Further and other objects of the invention will become apparent to those skilled in the art when considering the following summary of the invention and the more detailed description of the preferred embodiments illustrated herein.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 is a Bland-Altman plot showing the precision of the calculated oxygen consumption compared to the actual “oxygen consumption” simulation in a model, labeled as “virtual {dot over (V)}O₂”.

SUMMARY OF THE INVENTION

According to a primary aspect of the invention, there is provided a method to precisely calculate the flux of O₂ (VO₂) and anesthetic gases such as N₂O (VN₂O) during steady state low flow anesthesia with a semi-closed or dosed circuit such as a circle anesthetic circuit or the like. For our calculations, we require only the gas flow settings and the outputs of a tidal gas analyzer. We will consider a patient breathing via a circle circuit with fresh gas consisting of O₂ and/or air, with or without N₂O, entering the circuit at a rate substantially less than the minute ventilation ({dot over (V)}E). We will refer to the total fresh gas flow (FGF) as “source gas flow” (SGF). Our perspective throughout will be that the circuit is an extension of the patient and that under steady state conditions, the mass balance of the flux of gases with respect to the circuit is the same as the flux of gases in the patient.

We present an approach that increases the precision of gas flux calculations for determining gas pharmacokinetics during low flow anesthesia, one application of which is to institute CCA. According to one aspect of the invention there is provided a process for determining gas(x) consumption, wherein said gas(x) is selected from;

-   -   a) an anesthetic such as but not limited to;         -   i) N₂O;         -   ii) sevoflurane;         -   iii) isoflurane;         -   iv) halothane;         -   v) desflurame; or the like     -   b) Oxygen (O₂);

for example, in a semi-closed or closed circuit, or the like comprising the following relationships;

wherein said relationships are selected from the groups covering the following circumstances;

Model 1

As an initial simplifying assumption, we consider that the CO₂ absorber is out of the circuit and the respiratory quotient (RQ) is 1.

We can make a number of statements with regard to Model 1:

-   -   1) The flow of gas entering the circuit is SGF and the flow of         gas leaving the circuit is equal to SGF.     -   2) The gas leaving the circuit is predominantly alveolar gas.         This is substantially true as the first part of the exhaled gas         that contains anatomical dead-space gas would tend to bypass the         pressure relief valve and enter the reservoir bag. When the         reservoir bag is full, the pressure in the circuit will rise,         thereby opening the pressure relief valve, allowing the         later-expired gas from the alveoli to exit the circuit.     -   3) The volume of any gas ‘x’ entering the circuit can be         calculated by multiplying SGF times the fractional concentration         of gas x in SGF (FSX). The volume of gas x leaving the circuit         is SGF times the fractional concentration of x in end tidal gas         (FETX). The net volume of gas x absorbed by, or eliminated from,         the patient is SGF (FSX−FETX). For example, {dot over (V)}O₂=SGF         (FSO₂−FETO₂) where SGF and FSO₂ can be read from the flow meter         and FETO₂ is read from the gas monitor. Similar calculations can         be used to calculate {dot over (V)}CO₂ and the flux of inhaled         anesthetic agents.         Model 2

We will now consider a circle circuit with a CO₂ absorber in the circuit. As an initial simplifying assumption, we will assume that all of the expired gas passes through the CO₂ absorber and RQ is 1 (see FIG. 1 b).

With this model, all of the CO₂ produced by the patient is absorbed, so the total flow of gas out of the circuit (Tfout; equivalent to the expiratory flow, VE) is no longer equal to SGF but equal to SGF minus {dot over (V)}O₂. TFout=SGF−{dot over (V)}O₂   (1)

{dot over (V)}O₂ is calculated as the flow of O₂ into the circuit (O₂in; equivalent in standard terminology to VO₂in) minus the flow of O₂ out of the circuit (O₂out; equivalent in standard terminology to VO₂out). {dot over (V)}O₂=O₂in−O₂out   (2) Since, O₂out=TFout*FETO₂   (3) then simply by substituting (3) for O₂out in (2) we can calculate {dot over (V)}O₂ from the gas settings and the O₂ gas monitor reading: {dot over (V)}O₂═SGF*(FSO₂−FETO₂)/(1−FETO₂)   (4) Model 3

We will again consider the case of anesthesia provided via a circle circuit with a CO₂ absorber in the circuit. In this model we will take into account that some expired gas escapes through the pressure relief valve (FIG. 2) and some passes through the CO₂ absorber. The RQ is still assumed to be 1. We will ignore for the moment the effect of anatomical dead-space and assume all gas entering the patient contributes to gas exchange. We will assume that during inhalation the patient receives all of the SGF and the balance of the inhaled gas in the alveoli comes from the expired gas reservoir after being drawn through the CO₂ absorber.

An additional simplifying assumption is that the volume of gas passing through the CO₂ absorber is the difference between {dot over (V)}E and the SGF (i.e., {dot over (V)}_(E)−SGF)¹. The proportion of previous exhaled gas passing through the CO₂ absorber that is distributed to the alveoli is 1−SGF/{dot over (V)}E². We will call this latter proportion ‘a’. ¹ In fact, it is the {dot over (V)}E−SGF+{dot over (V)}CO₂ abs. The difference between this value and our assumption is so small that we will ignore it for now ² Why this is not strictly true is described in the discussion about Model 4; absorption of CO₂ increases the concentrations of other gases. a=1−SGF/{dot over (V)}E   (5)

As before, we know the flows and concentrations of gases entering the circuit. To calculate the flow of individual gases leaving the circuit we need to know the total flow of gas out of the circuit. In this model we account for the volume of CO₂ absorbed by the CO₂ absorber. We still assume RQ=1. The flow out of the circuit is equal to the SGF minus the {dot over (V)}O₂ plus the {dot over (V)}CO₂, minus the volume of CO₂ in the gas that is drawn through the CO₂ absorber ({dot over (V)}CO₂abs): Tfout=SGF−{dot over (V)}O₂+{dot over (V)}CO₂−{dot over (V)}CO₂abs   (6)

Recall that {dot over (V)}CO₂abs=a {dot over (V)}CO₂ TFout=SGF−{dot over (V)}O₂+{dot over (V)}CO₂ −a {dot over (V)}CO₂ {dot over (V)}O₂=O₂in−O₂ out {dot over (V)}O₂=O₂ in−(SGF−{dot over (V)}O₂+{dot over (V)}CO₂ −a {dot over (V)}CO₂)FETO₂

As the RQ is assumed to be 1, we can substitute {dot over (V)}O₂ for {dot over (V)}CO₂ and VE for VI and solve for {dot over (V)}O₂: $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{{O_{2}{in}} - {{SGF} \times F_{ET}O_{2}}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}E}} \right)F_{ET}O_{2}}}} & (7) \end{matrix}$

In addition, we amend the equations to account for the actual RQ, if known. When we assumed that RQ=1, we were able to simply substitute {dot over (V)}O₂ for {dot over (V)}CO₂. To correct for RQ other than 1, we now use {dot over (V)}CO₂=RQ*{dot over (V)}O₂ and {dot over (V)}CO₂ abs is therefore equal to a*RQ*VO₂. Therefore TFout=SGF−{dot over (V)}O₂+{dot over (V)}CO₂−{dot over (V)}CO₂abs   (6) becomes TFout=SGF−{dot over (V)}O₂+RQ {dot over (V)}O₂ −a*RQ*{dot over (V)}O₂   (8)

In the case of a second gas being absorbed, such as N₂O or anesthetic vapor, a similar equation can be written in which the total flow out (TFout) also includes a term correcting for the flux of N₂O ({dot over (V)}N₂O) and/or anesthetic agent (VAA).

Therefore for Model 3 with calculations of {dot over (V)}N₂O absorption ({dot over (V)}N₂O) and RQ=1

In model 3, adding terms for the calculation of {dot over (V)}N₂O to equation (6) while assuming RQ=1, TFout=SGF−{dot over (V)}O₂−{dot over (V)}N₂O+{dot over (V)}CO₂−{dot over (V)}CO₂abs   (AA1) In order to determine the {dot over (V)}N₂O, a second mass balance equation about the circuit with respect to N₂O is required. For {dot over (V)}CO₂abs=a*{dot over (V)}CO₂ and a=1−SGF/{dot over (V)}E {dot over (V)}N₂O=N₂O in−(SGF−{dot over (V)}O₂−{dot over (V)}N₂O+{dot over (V)}CO₂ −a*{dot over (V)}CO₂)*FETN₂O   (AA2)

As RQ is still assumed to equal 1, {dot over (V)}O₂={dot over (V)}CO₂ $\begin{matrix} \begin{matrix} {{\overset{.}{V}N_{2}O} = {{N_{2}O\quad{in}} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}\quad N_{2}\quad O} +} \\ {{\overset{\quad}{\overset{.}{V}}\quad O_{\quad 2}} - {a\overset{.}{V}O_{\quad 2}}} \end{pmatrix}*F_{ET}N_{\quad 2}O}}} \\ {= {{N_{2}O\quad i\quad n} - {\left( {{SGF} - {a\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O}} \right)*F_{ET}N_{2}O}}} \end{matrix} & \left( {{AA}\quad 3} \right) \end{matrix}$

Therefore when taking {dot over (V)}N₂O into account, {dot over (V)}O₂ can be recalculated as $\begin{matrix} \begin{matrix} {{\overset{.}{V}O_{2}} = {{O_{2}i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{\overset{.}{V}{CO}_{\quad 2}} - {a*\overset{.}{V}{CO}_{\quad 2}}} \end{pmatrix}*F_{ET}O_{2}}}} \\ {= {{O_{2}i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{\overset{.}{V}O_{\quad 2}} - {a\overset{.}{V}O_{\quad 2}}} \end{pmatrix}*F_{ET}O_{2}}}} \\ {= {{O_{2}i\quad n} - {\left( {{SGF} - {a\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O}} \right)*F_{ET}O_{2}}}} \end{matrix} & \left( {{AA}\quad 4} \right) \end{matrix}$ Basically, we have two equations, (AA3) and (AA4) with two unknowns, {dot over (V)}O₂ and {dot over (V)}N₂O. Solving equation (AA3) for {dot over (V)}N₂O, $\begin{matrix} {{\overset{.}{V}N_{2}O} = \frac{{N_{2}O\quad i\quad n} - {\left( {{SGF} - {a\overset{.}{V}O_{2}}} \right)*F_{ET}N_{2}O}}{1 - {F_{ET}N_{2}O}}} & \left( {{AA}\quad 5} \right) \end{matrix}$

Substituting (AA5) into equation (AA4) and solving for {dot over (V)}O₂, $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{{\left( {1 - {F_{ET}N_{2}O}} \right)*O_{2}i\quad n} - {\left( {{SGF} - {N_{2}O\quad i\quad n}} \right)*F_{ET}O_{2}}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}E}} \right)*F_{ET}O_{2}} - {F_{ET}N_{2}O}}} & \left( {{AA}\quad 6} \right) \end{matrix}$ And calculating {dot over (V)}N₂O taking into account {dot over (V)}O₂, CO₂ absorption and RQ=1: $\begin{matrix} {{\overset{.}{V}N_{2}O} = \frac{\begin{matrix} {{\left( {1 - {\left( {1 - \frac{SGF}{\overset{.}{V}E}} \right)*F_{ET}O_{2}}} \right)*N_{2}O\quad i\quad n} -} \\ {\left( {{SGF} - {O_{2}i\quad n}} \right)*F_{ET}N_{2}O} \end{matrix}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}E}} \right)*F_{ET}O_{2}} - {F_{ET}N_{2}O}}} & \left( {{AA}\quad 7} \right) \end{matrix}$ $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{\begin{matrix} {{\left( {1 - {F_{ET}N_{2}O} - {F_{ET}{AA}}} \right)*O_{2}i\quad n} -} \\ {\left( {{SGF} - {N_{2}O\quad i\quad n} - {{AA}\quad i\quad n}} \right)*F_{ET}O_{2}} \end{matrix}}{1 - {a*F_{ET}O_{2}} - {F_{ET}N_{2}O} - {F_{ET}{AA}}}} & \left( {{AA}\quad 8} \right) \\ {{\overset{.}{V}N_{2}O} = \frac{\begin{matrix} {{\left( {1 - {a*F_{ET}O_{2}} - {F_{ET}{AA}}} \right)*N_{2}O\quad i\quad n} -} \\ {\left( {{SGF} - {a*O_{2}i\quad n} - {{AA}\quad i\quad n}} \right)*F_{ET}N_{2}O} \end{matrix}}{1 - {a*F_{ET}O_{2}} - {F_{ET}N_{2}O} - {F_{ET}{AA}}}} & \left( {{AA}\quad 9} \right) \\ {{{\overset{.}{V}{AA}} = \frac{\begin{matrix} {{\left( {1 - {a*F_{ET}O_{2}} - {F_{ET}N_{2}O}} \right)*{AA}\quad i\quad n} -} \\ {\left( {{SGF} - {a*O_{2}i\quad n} - {N_{2}O\quad i\quad n}} \right)*F_{ET}{AA}} \end{matrix}}{1 - {a*F_{ET}O_{2}} - {F_{ET}N_{2}O} - {F_{ET}{AA}}}}{{{where}\quad a} = {1 - \frac{SGF}{\overset{.}{V}E}}}} & \left( {{AA}\quad 10} \right) \end{matrix}$ Model 3 with N2O, RQ

Taking into account the actual RQ while calculating {dot over (V)}N₂O, equation 9 becomes, TFout=SGF−{dot over (V)}O₂−{dot over (V)}N₂O+RQ {dot over (V)}O₂ −a*RQ* {dot over (V)}O₂   (AA11)

Therefore equation (AA2) becomes, {dot over (V)}N₂O=N₂O in −(SGF−{dot over (V)}O₂−{dot over (V)}N₂O+RQ {dot over (V)}O₂ −a*RQ*{dot over (V)}O₂)*FETN₂O   (AA12)

And equation (AA4) becomes, {dot over (V)}O₂=O₂in −(SGF−{dot over (V)}O₂−{dot over (V)}N₂O+RQ {dot over (V)}O₂ −a*RQ*{dot over (V)}O₂)*FETO₂   (AA13)

Now, we have two equations, (AA12) and (AA13) with two unknowns, {dot over (V)}O₂ and {dot over (V)}N₂O.

Solving equation (AA12) and (AA13) for {dot over (V)}O₂ and {dot over (V)}N₂O, $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{{\left( {1 - {F_{ET}N_{2}O}} \right)*O_{2}i\quad n} - {\left( {{SGF} - {N_{2}O\quad i\quad n}} \right)*F_{ET}O_{2}}}{1 - {b*F_{ET}O_{2}} - {F_{ET}N_{2}O}}} & \left( {{AA}\quad 14} \right) \\ {{\overset{.}{V}N_{2}O} = \frac{\begin{matrix} {{\left( {1 - {b*F_{ET}O_{2}}} \right)*N_{2}O\quad i\quad n} -} \\ {\left( {{SGF} - {O_{2}i\quad n}} \right)*F_{ET}N_{2}O} \end{matrix}}{1 - {b*F_{ET}O_{2}} - {F_{ET}N_{2}O}}} & \left( {{AA}\quad 15} \right) \end{matrix}$ where b is the fraction of the CO₂ production (VCO₂) passing through the CO₂ absorber. “b” is analogous to “a” and is formulated to account for the actual RQ. $b = {{1 - {{RQ}\left( {1 - \left( {1 - \frac{SGF}{\overset{.}{V}E}} \right)} \right)}} = {1 - {{RQ}*\frac{SGF}{\overset{.}{V}E}}}}$ Model 3 with N₂O and Anesthetic Agent, RQ

Similarly, the flux of gases can be calculated taking into account the actual RQ. $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{\begin{matrix} {{\left( {1 - {F_{ET}\quad N_{2}O} - {F_{ET}{AA}}} \right)*O_{2}i\quad n} -} \\ {\left( {{SGF} - {N_{2}O\quad i\quad n} - {{AA}\quad i\quad n}} \right)*F_{ET}O_{2}} \end{matrix}}{1 - {b*F_{ET}\quad O_{2}} - {F_{ET}\quad N_{2}O} - {F_{ET}{AA}}}} & ({AA16}) \\ {{{\overset{.}{V}N_{2}O} = \frac{\begin{matrix} {{\left( {1 - {b*F_{ET}O_{2}} - {F_{ET}{AA}}} \right)*N_{2}O\quad i\quad n} -} \\ {\left( {{SGF} - {b*O_{2}i\quad n} - {{AA}\quad i\quad n}} \right)*F_{ET}N_{2}O} \end{matrix}}{1 - {b*F_{ET}O_{2}} - {F_{ET}N_{2}O} - {F_{ET}{AA}}}}{{\overset{.}{V}{AA}} = \frac{\begin{matrix} {{\left( {1 - {b*F_{ET}O_{2}} - {F_{ET}N_{2}O}} \right)*{AA}\quad i\quad n} -} \\ {\left( {{SGF} - {b*O_{2}i\quad n} - {N_{2}O\quad i\quad n}} \right)*F_{ET}{AA}} \end{matrix}}{1 - {b*F_{ET}O_{3}} - {F_{ET}N_{2}O} - {F_{ET}{AA}}}}} & ({AA17}) \end{matrix}$ Model 4

The one remaining simplifying assumption is that we have ignored the effects of the anatomical dead-space.

We know the portion of the inspired gas that passes through the CO₂ absorber as {dot over (V)}E-SGF. However, the net amount of CO₂ absorbed by the CO₂ absorber will be equal to that contained in the portion of the {dot over (V)}E-SGF that originated from the alveoli on a previous breath. The gas from the alveoli has a FCO₂ equal to FETCO₂. Therefore, the proportion of inhaled gas drawn through the CO₂ absorber we had previously designated as ‘a’ is actually equal to 1−SGF/{dot over (V)}A. To avoid confusion in subsequent derivations we will designate 1−SGF/{dot over (V)}A as a′.

We now amend equation (7) removing simplifying assumptions about RQ and using a′ as the proportion of gas passing the CO₂ absorber.

Now, {dot over (V)}O₂abs=a*{dot over (V)}O₂=(1−SGF/{dot over (V)}A)*{dot over (V)}O₂   (9)

From equation (8), $\begin{matrix} \begin{matrix} {{TFout} = {{SGF} - {\overset{.}{V}O_{2}} + {\overset{.}{V}{CO}_{2}} - {\overset{.}{V}{CO}_{2}{abs}}}} \\ {= {{SGF} - {\overset{.}{V}O_{2}} + {\left( {1 - a^{\prime}} \right)*\overset{.}{V}{CO}_{2}}}} \\ {= {{SGF} - {\overset{.}{V}O_{2}} + {\left( {1 - \left( {1 - {{SGF}/{\overset{.}{V}}_{A}}} \right)} \right)*\overset{.}{V}{CO}_{2}}}} \\ {= {{SGF} - {\overset{.}{V}O_{2}} + {\left( {{{SGF}/\overset{.}{V}}A} \right)*\overset{.}{V}{CO}_{2}}}} \\ {= {{SGF} - {\overset{.}{V}O_{2}} + {{SGF}*\left( {\overset{.}{V}{{CO}_{2}/{\overset{.}{V}}_{A}}} \right)}}} \end{matrix} & (10) \end{matrix}$

As the standard definition of FETCO₂ is {dot over (V)}CO₂/{dot over (V)}A, we substitute {dot over (V)}CO₂/{dot over (V)}A for FETCO₂ in (10) ${TFout} = {{SGF} - {\overset{.}{V}O_{2}} + {{SGF}*{FET}\quad{CO}_{2}}}$ $\begin{matrix} {{\overset{.}{V}O_{2}} = {{O_{2}i\quad n} - {{TFout}*{FET}\quad O_{2}}}} \\ {= {{O_{2}i\quad n} - {\left( {{SGF} - {\overset{.}{V}O_{2}} + {{SGF}*{FET}\quad{CO}_{2}}} \right)*{FET}\quad O_{2}}}} \end{matrix}$

After isolating {dot over (V)}O2 $\begin{matrix} {{{VO}\quad 2} = \frac{{O\quad 2i\quad n} - {\left( {{SGF} + {{SGF}*{FET}\quad{CO}\quad 2}} \right)*{FET}\quad O_{2}}}{1 - {{FET}\quad O_{2}}}} & (11) \end{matrix}$ Model 4 Amended for VN2O

Amending equation (11) for {dot over (V)}N₂O TFout=SGF−{dot over (V)}O₂−{dot over (V)}N₂O+{dot over (V)}CO₂−{dot over (V)}CO₂abs

In order to determine the {dot over (V)}N₂O, a second mass balance about N2O is required: where {dot over (V)}CO₂abs=a′*{dot over (V)}CO₂ and a′=1−SGF/{dot over (V)}A $\begin{matrix} \begin{matrix} {{\overset{.}{V}N_{2}O} = {{N_{2}O\quad i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{\overset{.}{V}{CO}_{2}} - {a^{\prime}*\overset{.}{V}{CO}_{2}}} \end{pmatrix}*F_{ET}N_{2}O}}} \\ {= {{N_{2}O\quad i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {\left( {1 - a^{\prime}} \right)*\overset{.}{V}{CO}_{2}} \end{pmatrix}*F_{ET}N_{2}O}}} \\ {= {{N_{2}O\quad i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ \left( {1 - {\left( {1 - {{SGF}/{\overset{.}{V}}_{A}}} \right)*\overset{.}{V}{CO}_{2}}} \right) \end{pmatrix}*F_{ET}N_{2}O}}} \\ {= {{N_{2}O\quad i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{{SGF}/{\overset{.}{V}}_{A}}*\overset{.}{V}{CO}_{2}} \end{pmatrix}*F_{ET}N_{2}O}}} \\ {= {{N_{2}O\quad i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{SGF}*F_{ET}{CO}\quad 2} \end{pmatrix}*F_{ET}N_{2}O}}} \end{matrix} & (28) \end{matrix}$ In the same way, $\begin{matrix} \begin{matrix} {{\overset{.}{V}O_{2}} = {{O_{2}i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{\overset{.}{V}{CO}_{2}} - {a^{\prime}*\overset{.}{V}{CO}_{2}}} \end{pmatrix}*F_{ET}O_{2}}}} \\ {= {{O_{2}i\quad n} - {\begin{pmatrix} {{SGF} - {\overset{.}{V}O_{2}} - {\overset{.}{V}N_{2}O} +} \\ {{SGF}*F_{ET}{CO}\quad 2} \end{pmatrix}*F_{ET}O_{2}}}} \end{matrix} & (29) \end{matrix}$ Now, we have two equations, (28) and (29) with two unknowns, {dot over (V)}O₂ and {dot over (V)}N₂O. Solving equation (28) and (29) for {dot over (V)}O₂ and {dot over (V)}N₂O, $\begin{matrix} {{\overset{.}{V}O_{2}} = \frac{\begin{matrix} {{O_{2}i\quad n*\left( {1 - {F_{ET}N_{2}O}} \right)} -} \\ {\left( {{{SGF}*\left( {1 + {F_{ET}{CO}_{2}}} \right)} - {N_{2}O\quad i\quad n}} \right)*} \\ {F_{ET}O_{2}} \end{matrix}}{1 - {{FET}\quad N_{2}O} - {{FET}\quad O_{2}}}} & (30) \\ {{\overset{.}{V}N_{2}O} = \frac{\begin{matrix} {{N_{2}O\quad i\quad n*\left( {1 - {F_{ET}O_{2}}} \right)} -} \\ {\left( {{{SGF}*\left( {1 + {F_{ET}{CO}_{2}}} \right)} - {O\quad i\quad n}} \right)*} \\ {F_{ET}N_{2}O} \end{matrix}}{1 - {F_{ET}N_{2}O} - {F_{ET}O_{2}}}} & (31) \end{matrix}$

Note that RQ and {dot over (V)}A are not required to calculate flux. We present the equations where equation 11 is further amended to take into account {dot over (V)}N₂O and {dot over (V)}AA. $\begin{matrix} {{{\overset{.}{V}O\quad 2} = \frac{\begin{matrix} {O\quad 2\quad{{in}^{*}\left( {1 - {{FET}_{2}{NO}} - {{FETAAFET}_{2}{NO}^{*}{FETAA}_{2}}} \right)}} \\ \left( {{{SGF}^{*}\left( {1 + {{FET}_{2}{CO}}} \right)} - {N_{2}{Oin}} -} \right. \\ {{AAin}_{2}{FET}_{2}{NO}^{*}{{FETAA}^{*}\left( {1 -} \right.}} \\ {\left. \left. {{N_{2}{Oin}} - {AAin}} \right)^{*} \right){FET}_{2}O} \end{matrix}}{\begin{matrix} {\left( {1 - {{FET}_{2}{NO}}} \right)^{*}\left( {1 - {FETAA}_{2}} \right)} \\ {\left( {1 - {{FET}_{2}{NO}^{*}{FETAA}^{*}}} \right){FET}_{2}O} \end{matrix}}}{{VNO} = \frac{\begin{matrix} {{N_{2}{{Oin}^{*}\left( {1 - {{FET}_{2}O} - {FETAA} - {{FET}_{2}O^{*}{FETAA}}} \right)}} -} \\ \left( {{{SGP}^{*}\left( {1 + {{FET}_{2}{CO}}} \right)} - {O_{2}{in}} - {AAin} -} \right. \\ {\left. {{FET}_{2}O^{*}{{FETAA}^{*}\left( {1 - {O_{2}{in}} - {AAin}} \right)}^{*}} \right){FET}_{2}N\text{?}} \end{matrix}}{\begin{matrix} {{\left( {1 - {{FET}_{2}O}} \right)^{*}\left( {1 - {FETAA}} \right)} -} \\ {\left( {1 - {{FET}_{2}O^{*}{FETAA}}} \right)^{*}{FET}_{2}{NO}} \end{matrix}}}{\text{?}\text{indicates text missing or illegible when filed}}} & (11) \end{matrix}$ Model 4 with N2O and Anesthetic Agent

Similarly, the flux of additional anesthetic agents can be calculated by adding more $\begin{matrix} {{{\overset{.}{V}O\quad 2} = \frac{\begin{matrix} {O\quad 2\quad{{in}^{*}\left( {1 - {{FET}_{2}{NO}} - {{FETAAFET}_{2}{NO}^{*}{FETAA}_{2}}} \right)}} \\ \left( {{{SGF}^{*}\left( {1 + {{FET}_{2}{CO}}} \right)} - {N_{2}{Oin}} -} \right. \\ {{AAin}_{2}{FET}_{2}{NO}^{*}{{FETAA}^{*}\left( {1 -} \right.}} \\ {\left. \left. {{N_{2}{Oin}} - {AAin}} \right)^{*} \right){FET}_{2}O} \end{matrix}}{\begin{matrix} {\left( {1 - {{FET}_{2}{NO}}} \right)^{*}\left( {1 - {FETAA}_{2}} \right)} \\ {\left( {1 - {{FET}_{2}{NO}^{*}{FETAA}^{*}}} \right){FET}_{2}O} \end{matrix}}}{{VNO} = \frac{\begin{matrix} {{N_{2}{{Oin}^{*}\left( {1 - {{FET}_{2}O} - {FETAA} - {{FET}_{2}O^{*}{FETAA}}} \right)}} -} \\ \left( {{{SGP}^{*}\left( {1 + {{FET}_{2}{CO}}} \right)} - {O_{2}{in}} - {AAin} -} \right. \\ {\left. {{FET}_{2}O^{*}{{FETAA}^{*}\left( {1 - {O_{2}{in}} - {AAin}} \right)}^{*}} \right){FET}_{2}N\text{?}} \end{matrix}}{\begin{matrix} {{\left( {1 - {{FET}_{2}O}} \right)^{*}\left( {1 - {FETAA}} \right)} -} \\ {\left( {1 - {{FET}_{2}O^{*}{FETAA}}} \right)^{*}{FET}_{2}{NO}} \end{matrix}}}{{\overset{.}{V}{AA}} = \frac{\begin{matrix} {{{AAin}^{*}\left( {1 - {{FET}_{2}{NO}} - {{FET}_{2}O} - {{FET}_{2}{NO}^{*}{FET}_{2}O}} \right)} -} \\ \left( {{{SGF}^{*}\left( {1 + {{FET}_{2}{CO}}} \right)} - {N_{2}{Oin}} - {O_{2}{in}} -} \right. \\ {\left. {{FET}_{2}{NO}^{*}{FET}_{2}{O^{*}\left( {1 - {N_{2}{Oin}} - {O_{2}{in}}} \right)}} \right)^{*}{FETAA}} \end{matrix}}{\begin{matrix} {{\left( {1 - {{FET}_{2}{NO}}} \right)^{*}\left( {1 - {{FET}_{2}O}} \right)} -} \\ {\left( {1 - {{FET}_{2}{NO}^{*}{FET}_{2}O}} \right)^{*}{FETAA}} \end{matrix}}}{\text{?}\text{indicates text missing or illegible when filed}}} & \quad \end{matrix}$ Advantages of this method compared to the prior art:

In our method compared to Severinghause (#2)

-   -   iv) Patients are maintained with low fresh gas flows (FGF) in a         semi-closed circuit, the commonest method of providing         anesthesia. No further manipulations by the anesthetist are         required.     -   v) Method uses information normally available in the operating         room without additional equipment or monitors.     -   vi) The calculations can be made with any flow, or combination         of flows, of O₂ and N₂O.     -   vii) Patients can be ventilated or be breathing spontaneously.     -   viii) Our method can be used to calculate low rates of         uptake/absorption such as those of anesthetic vapors Compared to         metabolic carts, our method, does not require equipment on         addition to that required to anesthetize the patient and there         is no need to collect exhaled gas or gas leaving the circuit.

Our method does not require breathing an externally supplied tracer gas. We monitor only routinely available information such as the settings of the O₂ and N₂O flowmeters and the concentrations of gases in expired gas as measured by the standard operating room gas monitor.

Compared to Biro, our approach: VO₂=O₂in−O₂out (where O₂in and O₂out are O₂out=TFout*FETO₂ TFout=TFin−VO₂ VO₂=O₂in−(TFin−VO₂)*FETO₂

Solving for {dot over (V)}O₂ VO₂=(O₂in−TFin*FETO₂)/1−FETO₂ where

-   -   {dot over (V)}O₂ is oxygen consumption     -   TFin is total flow of gas entering the circuit (equivalent to         inspiratory flow, VI)     -   TFout is total flow of gas leaving the circuit (equivalent to         expiratory flow, VE)     -   O₂Out is total flow of O₂ leaving the circuit (equivalent to         VO₂out)     -   O₂in is total flow of O₂ entering the circuit (equivalent to         VO₂in)     -   FETO₂ is the fractional concentration of O₂ in the expired         (end-tidal) gas

Our equation takes the same form as that presented by Biro except that Biro's has FIO₂ instead of FETO₂ in analogous places in the numerator and denominator of the term on the right side of the equation. This will clearly result in different values for VO₂ compared to our method. In addition, the difference is that FETO₂ is a steady number during the alveolar phase of exhalation and therefore can be measured and its value is representative of alveolar gas whereas FIO₂ is not a steady number; FIO₂ varies during inspiration and no value at any particular time during inspiration is representative of inspired gas.

Compared to Viale, our method does not require FIO₂, FEN₂, FIN₂ or the patient's gas flows.

Compared to Bengston, our method does not require knowledge of the patient's weight or duration of anesthesia. Our method can be performed with any ratio of O₂/N₂O flow into the circuit. Our method does not require expired gas collection or measurements of gas volume.

Compared to methods by Lowe, Lin or Pestana, our method uses only routinely available information such as the flowmeter settings and end tidal O₂ concentrations. It does not require any invasive procedures.

With these equations, the limiting factor for the precise calculation of gas fluxes is the precision of flowmeters and monitors on anesthetic machines. In addition, leaks, if any, from the circuit and the sampling rate of the gas monitor must be known and taken into account in the calculation. As commercial anesthetic machines are not built to such specifications, we constructed an “anesthetic machine” with precise flowmeters and a lung/circuit model with precisely known flows of O₂ and CO₂ leaving and entering the circuit respectively. We then compared the known fluxes of O₂ and CO₂ with that calculated from the SGF, minute ventilation and the gas concentrations as analyzed by a gas monitor. FIG. 1 shows the Bland-Altman analysis of the results. 

1) A precise method for determining gas flux calculations and gas pharmacokinetics during low flow anesthesia, one example of which is to institute for dosed circuit anesthesia and for example for a process for determining gas(x) consumption, wherein said gas(x) is selected from; a) an anesthetic such as but not limited to; i) N₂O; ii) sevoflurane; iii) isoflurane; iv) halothane; v) desflurame; or the like b) Oxygen (O₂); and further comprising the relationships described in relation to Models I to IV and variations thereof described in the disclosure. 2) A method of determining oxygen consumption, and/or CO₂ production in a subject breathing via a partial rebreathing circuit by the use of information derived from gas flow and composition of gas entering a partial rebreathing circuit and tidal monitor gas concentration readings. 3) A method of determining of oxygen consumption, anesthetic gas absorption and CO₂ production in a subject breathing via a partial rebreathing circuit by the use of information derived from gas flow and composition of gas entering a partial rebreathing circuit and tidal monitor gas concentration readings. 4) The method of claim 2 where the circuit is a circle anesthetic circuit or any anesthetic circuit with CO₂ absorber in the circuit 5) The method of claim 3 where the circuit is a circle anesthetic circuit or any anesthetic circuit with CO₂ absorber in the circuit 6) The process of claim 1 with the use of any of the equations disclosed herein in models 14, including any of the intermediate equations used. 7) Use of any of the following equations or their intermediate equations, for determination of {dot over (V)}O₂ $\begin{matrix} {{\overset{.}{V}O_{2}} = {{SGF}*{\left( {{FsO}_{2} - {FETO}_{2}} \right)/\left( {1 - {FETO}_{2}} \right)}}} & (4) \\ {{\overset{.}{V}\quad O_{2}} = \frac{{O_{2}{in}} - {{SGF} \times {FETO}_{2}}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right){FETO}_{2}}}} & (7) \\ {{\overset{.}{V}\quad O_{2}} = \frac{{\left( {1 - {{FETN}_{2}O}} \right)*O_{2}{in}} - {\left( {{SGF} - {N_{2}{Oin}}} \right)*{FETO}_{2}}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right)*{FETO}_{2}} - {{FETN}_{2}O}}} & ({AA6}) \\ {{\overset{.}{V}\quad O_{2}} = \frac{{\left( {I - {{FETN}_{2}O} - {FETAA}} \right)*O_{2}{in}} - {\left( {{{SGF\_ N}_{2}{Oin}} - {AAin}} \right)*{FETO}_{2}}}{1 - {a*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}} & ({AA8}) \\ {{\overset{.}{V}\quad O_{2}} = \frac{{\left( {1 - {{FETN}_{2}O} - {FETAA}} \right)*O_{2}{in}} - {\left( {{SGF} - {N_{2}{Oin}} - {AAin}} \right)*{FETO}_{2}}}{1 - {b*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}} & ({AA16}) \\ {{{VO}\quad 2} = \frac{{O\quad 2{in}} - {\left( {{SGF} + {{SGF}*{FETCO}\quad 2}} \right)*{FETO}_{2}}}{1 - {FETO}_{2}}} & (11) \\ {{\overset{.}{V}\quad O_{2}} = \frac{\begin{matrix} {{O_{2}{in}*\left( {1 - {{FETN}_{2}O}} \right)} -} \\ {\left( {{{SGF}*\left( {1 + {FETCO}_{2}} \right)} - {N_{2}{Oin}}} \right)*{FETO}_{2}} \end{matrix}}{1 - {{FETN}_{2}O} - {FETO}_{2}}} & (30) \\ {{{\overset{.}{V}\quad O\quad 2} = \frac{\begin{matrix} {O\quad 2{{in}\left( {1 - {{FETN}_{2}O} - {{FETAAFETN}_{2}O*{FETAA}}} \right)}} \\ {\left( {{{SGF}\left( {1 + {FETCO}} \right)} - {N_{2}{Oin}} - {AAinFETN}_{2}} \right)*} \\ {{FETAA}\left( {1 - {N_{2}{Oin}} - {AAin}} \right){FETO}} \end{matrix}}{\left( {1 - {{FETN}_{2}O}} \right)*\left( {1 - {FETAA}} \right)\left( {1 - {{FETN}_{2}O*{FETAA}}} \right){FETO}_{2}}}{{\overset{.}{V}\quad O\quad 2} = \frac{\begin{matrix} {O_{2}{in}*} \\ {\left( {1 - {{FETN}_{2}O} - {FETAA} - {{FETN}_{2}O*{FETAA}}} \right) -} \\ \left( {{{SGF}*\left( {1 + {FETCO}_{2}} \right)} - {N_{2}{Oin}} - {AAin} -} \right. \\ {{FETN}_{2}O*{FETAA}*\left( {1 - {N_{2}{Oin}} - {AAin}} \right)} \end{matrix}}{\begin{matrix} {{\left( {1 - {{FETN}_{2}O}} \right)*\left( {1 - {FETAA}} \right)} -} \\ {\left( {1 - {{FETN}_{2}O*{FETAA}}} \right)*{FETO}_{2}} \end{matrix}}}} & (11) \end{matrix}$ 8) Use of any of the following equations or their intermediate equations, for determination of {dot over (V)}N₂O $\begin{matrix} {{\overset{.}{V}\quad N_{2}O} = \frac{{N_{2}{Oin}} - {\left( {{SGF} - {a\quad\overset{.}{V}\quad O_{2}}} \right)*{FETN}_{2}O}}{1 - {{FETN}_{2}O}}} & ({AA5}) \\ {{\overset{.}{V}\quad N_{2}O} = \frac{\begin{matrix} {{\left( {1 - {\left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right)*{FETO}_{2}}} \right)*N_{2}{Oin}} -} \\ {\left( {{SGF} - {O_{2}{in}}} \right)*{FETN}_{2}O} \end{matrix}}{1 - {\left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right)*{FETO}_{2}} - {{FETN}_{2}O}}} & ({AA7}) \\ {{\overset{.}{V}\quad N_{2}O} = \frac{{\left( {1 - {a*{FETO}_{2}} - {FETAA}} \right)*N_{2}{Oin}} - {\left( {{SGF} - {a*O_{2}{in}} - {AAin}} \right)*{FETN}_{2}O}}{1 - {a*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}} & ({AA9}) \\ {{{\overset{.}{V}\quad N_{2}O} = \frac{{\left( {1 - {b*{FETO}_{2}}} \right)*N_{2}{Oin}} - {\left( {{SGF} - {O_{2}{in}}} \right)*{FETN}_{2}O}}{1 - {b*{FETO}_{2}} - {{FETN}_{2}O}}}{{Where}\quad b} = {{1 - {{RQ}\left( {1 - \left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right)} \right)}} = {1 - {{RQ}*\frac{SGF}{\overset{.}{V}\quad E}}}}} & ({AA15}) \\ {{{\overset{.}{V}\quad N_{2}O} = \frac{{\left( {1 - {b*{FETO}_{2}} - {FETAA}} \right)*N_{2}{Oin}} - {\left( {{SGF} - {b*O_{2}{in}} - {AAin}} \right)*{FETN}_{2}O}}{1 - {b*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}}{{VNO} = \frac{\begin{matrix} {N_{2}{Oin}*} \\ {\left( {1 - {FETO}_{2} - {FETAA} - {{FETO}_{2}*{FETAA}}} \right) -} \\ \begin{pmatrix} {{{SGF}\left( {1 + {FETCO}_{2}} \right)} - {O_{2}{in}} - {AAin} -} \\ {{FETO}_{2}*{FETAA}*\left( {1 - {O_{2}{in}} - {AAin}} \right)} \end{pmatrix} \\ {{FETN}_{2}O} \end{matrix}}{\begin{matrix} {{\left( {1 - {FETO}_{2}} \right)*\left( {1 - {FETAA}} \right)} -} \\ {\left( {1 - {{FETO}_{2}*{FETAA}}} \right)*{FETN}_{2}O} \end{matrix}}}} & ({AA17}) \end{matrix}$ 9) Use of any of the following equations or their intermediate equations, for determination of {dot over (V)}AA $\begin{matrix} {{{\overset{.}{V}\quad{AA}} = \frac{{\left( {1 - {a*{FETO}_{2}} - {{FETN}_{2}O}} \right)*{AAin}} - {\left( {{SGF} - {a*O_{2}{in}} - {N_{2}{Oin}}} \right)*{FETAA}}}{1 - {a*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}}{{{where}\quad a} = {1 - \frac{SGF}{\overset{.}{V}\quad E}}}{{\overset{.}{V}\quad{AA}} = \frac{{\left( {1 - {b*{FETO}_{2}} - {{FETN}_{2}O}} \right)*{AAin}} - {\left( {{SGF} - {b*O_{2}{in}} - {N_{2}{Oin}}} \right)*{FETAA}}}{1 - {b*{FETO}_{2}} - {{FETN}_{2}O} - {FETAA}}}{{{Where}\quad b} = {{1 - {{RQ}\left( {1 - \left( {1 - \frac{SGF}{\overset{.}{V}\quad E}} \right)} \right)}} = {1 - {{RQ}*\frac{SGF}{\overset{.}{V}\quad E}}}}}{{\overset{.}{V}\quad{AA}} = \frac{\begin{matrix} {{AAin}*} \\ {\left( {1 - {FETNO} - {FETO} - {{FETNO}*{FETO}}} \right) -} \\ {\begin{pmatrix} {{{SGF}*\left( {1 + {FETCO}} \right)} - {N_{2}{Oin}} - {O_{2}{in}} -} \\ {{FETNO}*{FETO}*\left( {1 - {N_{2}{Oin}} - {O_{2}{in}}} \right)} \end{pmatrix}*} \\ {FETAA} \end{matrix}}{\begin{matrix} {{\left( {1 - {FETNO}} \right)*\left( {1 - {FETO}} \right)} -} \\ {\left( {1 - {{FETNO}*{FETO}}} \right)*{FETAA}} \end{matrix}}}} & ({AA10}) \end{matrix}$ 